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双语推荐:碳酸二乙酯

在101.325 kPa下,测定了碳酸二-碳酸二乙酯二元体系在不同平衡温度时的汽相和液相的折光率,并用事先测定的工作曲线拟合得到汽、液相的摩尔分率,用积分检验法检验其热力学一致性;用最小乘法分别求出了碳酸二-碳酸二乙酯二元体系的液相活度系数Wilson,NRTL和UNIQUAC模型参数,由这些模型参数推算的结果与实验数据吻合很好。
Refractive indexes of vapor phase and liquid phase in the binary system of dimethyl carbonate (DMC)-diethyl carbonate (DEC) at different equilibrium temperature under 101.325 kPa were determined. Vapor-Liquid mole fraction was got with working curve fitting, integral testing was used to test the thermodynamic consistency; liquid activity coefficient of Wilson, NRTL and UNIQUAC model parameters was obtained by using the method of least squares, the results could well correlate with experimental results.

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碳酸二(DMC)与醇进行交换法合成碳酸二乙酯(DEC),并考察不同催化剂、催化剂用量、反应时间、反应配比、催化剂重复性使用对反应的影响.结果表明,无水硝酸镧催化碳酸二醇的交换反应具有优良的活性;当反应温度为76-80℃,醇与DMC摩尔比为8∶1,催化剂用量占DMC量的0.7%(摩尔分数)时,反应7h后DMC的转化率为86.0%,碳酸二乙酯碳酸乙酯(EMC)的产率分别为59%和26.5%,交换反应的选择性为99.4% ;催化剂无水硝酸镧在重复使用5次后仍具有很好的催化活性.
T his paper studies the synthesis of diethyl carbonate by the transesterification of dimethyl carbonate (DMC) with ethanol .It finds that lanthanum nitrate is a good catalyst for this reaction . The reaction conditions are optimized .When the temperature is between 76 and 80 ℃ ,n(ethanol)∶n(DMC)=8∶1 ,the amount of catalyst is 0 .7 mol% of DMC ,the conversion of DMC after 7 hours of reaction is 86 .0% and the yields of diethyl carbonate (DEC) and ethyl methyl carbonate (EMC) are 59% and 26 .5% ,respectively .The transesterification selectivity is 99 .4% .La(NO3 )3 has been re-used 5 times for the transesterification of DMC with ethanol without displaying loss of its catalytic ac-tivity .

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研究了以聚丙烯酸树为成膜物质与碳酸二等溶剂制备油墨,并对油墨性能进行。研究发现,在固含量低于40%的条件下,碳酸二与甲苯重量比为1:1的混合溶剂的溶解效果比单独溶剂更好。采用碳酸二、甲基环己烷和乙酯混合溶剂制备的无苯聚丙烯酸型油墨,油墨溶剂残留极低,油墨粘度(涂4#杯)15~30 s,细度小于20μm,初干性小于45 mm/30 s,附着牢度大于95%,性能优良。
Ink was prepared using polyacrylic resin as a film -former and solvents such as dimethyl carbonate.Performance of the ink was analyzed.The results indicated that under the condition of the solid content was lower than 40%, the dissolving effect of the mixed solvent ( dimethyl carbonate with toluene weight ratio 1:1 ) was better than either separate solvent.Non-benzene polyacrylic resin type ink prepared with dimethyl carbonate , methyl cyclohexane and ethyl acetate mixed solvent had a high performance that the solvents residue was extremely low , the viscosity ( 4#cup) was 15~30 s, the fineness was less than 20 μm, the initial dryness was less than 45 mm/30 s, and the adhesion was more than 95%.

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为了提高碳酸二乙酯的转化率与选择性,对氧化碳和醇直接合成碳酸二乙酯的过程进行了研究。确定了较优的催化剂为ZrO2和3 A分子筛作为混合催化剂。对催化剂的制备工艺进行了优化:采用正相沉淀方式,沉淀pH值为9,焙烧温度为600℃时制备的ZrO2按质量比为5∶2的比例与3 A分子筛进行物理混合后催化效果最佳。在醇和氧化碳的进料比为514/225 mmol下,碳酸二乙酯的产量可以达到0.0543 mmol,选择性在60%以上。在该催化体系中,加入脱水剂烯、环氧丙烷和环氧丁烷均无法达到高效提高反应产率的效果。
The catalyst used in synthesis of diethyl carbonate (DEC)from CO2 and ethanol was studied in order to improve the production and selectivity.The mixture of zirconium oxide (ZrO2 ) and 3 A molecular sieves was selected as the optimal catalyst.The preparation methods of catalysts were also optimized.ZrO2 was obtained by the precipitation method at pH=9 and then calcined at 600 ℃.ZrO2 and 3 A molecular sieves were mixed as the mass ratio of 5∶2.When the feed ratio of CO2 and ethanol was 51 4/225 mmol,the yield of DEC could reach 0.054 3 mmol with the selectivity of more than 60%.In the catalytic system,adding dehydrating agent into the reaction can not efficiently improve the reaction yield.

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在间歇反应釜内,以甲醇钠为催化剂,对碳酸二交换合成碳酸二乙酯反应进行了研究,考察了催化剂浓度、反应温度、醇与碳酸二的摩尔配比等因素对交换反应的影响,通过数据校正优化了实验原始数据,建立了动力学模型并进行严格的模型检验,得到了可靠的模型参数。结果表明,该反应为连串反应,中间产物为碳酸乙酯,反应焓分别为ΔH10=-1.595 kJ?mol-1,ΔH20=0.809 kJ?mol-1;两个反应均为可逆反应,活化能分别为Ea1+=45.633 kJ?mol-1和Ea1-=47.228 kJ?mol-1、Ea2+=55.058 kJ?mol-1和Ea2-=54.249 kJ?mol-1。
The synthesis of diethyl carbonate using dimethyl carbonate and ethanol and catalyzed by sodium methoxide was studied experimentally in a batch stirred tank reactor. The effects of catalyst dosage, temperature, and molar ratio of ethanol to dimethyl carbonate on trans-esterification were investigated. A kinetic mathematical model was built to describe the reaction. It is found that the reaction consists two parts, and the intermediate product is methyl ethyl carbonate. The reaction heat is -1.595kJ?mol-1 for the first trans-esterification reaction and 0.809 kJ?mol-1 for the second one. Both of them are reversible. The forward and reverse activation energies of the first reaction are 45.633 kJ?mol-1 and 47.228 kJ?mol-1, respectively, while the second one shows that of 55.058 kJ?mol-1 and 54.249 kJ?mol-1, respectively.

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以碱性离子液体为催化剂,对碳酸二(DMC)和碳酸二乙酯(DEC)交换反应合成碳酸乙酯进行了研究.筛选出高催化活性的碱性离子液体1‐丁基‐3甲基咪唑丁酸盐([C4 mim][CH3(CH2)2 COO])为催化剂,详细考察了反应时间、温度、催化剂用量、原料配比等因素对交换反应的影响.实验结果表明,在反应温度为90℃,催化剂用量为6%(占反应物总质量百分数),n(DMC)∶ n(DEC)=1.5∶1,反应时间为5 h 时,DEC 的转化率高达48%.[C4 mim][CH3(CH2)2 COO]重复利用5次后仍保持较高的催化活性.
The synthesis of ethyl methyl carbonate (EMC) by transesterification of dimethyl carbonate (DMC) and diethyl carbonate (DEC) in the presence of alkaline ionic liquids as cata‐lysts was studied ,in which alkaline ionic liquid 1‐butyl‐3‐methylimidazolium butyrate ([C4 mim][CH3 (CH2 )2 COO ]) was selected due to its good catalytic performance compared with other alkaline ionic liquids .The effects of reaction time ,temperature ,catalyst loading and mo‐lar ratio of reactants on the conversion of the DEC were examined .Under the suitable reaction conditions of reaction temperature 90 ℃ ,catalyst dosage 6% (based on the total mass of the re‐actants) ,n(DMC) ∶ n(DEC) = 1 .5 ∶ 1 ,reaction time 5 h ,the conversion of DEC was 48% . After alkaline ionic liquid [C4 mim ][CH3 (CH2 )2 COO ] was recovered and reused five times without obvious loss of its catalytic activity .

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以γ-丁内为原料,分别与碳酸二碳酸二乙酯,在氢化钠的催化下,利用α氢的活泼性制得α-甲氧甲酰基-γ-丁内和α-氧甲酰基-γ-丁内。探索了反应温度、反应时间、反应物配比、催化剂用量对产率的影响。结果表明,适宜的反应条件为:①合成α-甲氧甲酰基-γ-丁内反应温度25℃,催化剂0.3 mol,反应时间3 h,反应物料物质的量比1∶1.5,产率可达85%;②合成α-氧甲酰基-γ-丁内反应温度30℃,催化剂0.3 mol,反应时间4 h,反应物物质的量比1∶2,产率可达76%。对产品进行了核磁共振氢谱、红外光谱表征。
α-Methoxyformyl-γ-butyrolactone and α-carbethoxy-γ-butyrolactone were synthesized usingγ-butyrolactone as raw material with dimethyl carbonate and diethyl carbonate by the chemical activity ofα-hydrogen under sodium hydride respectively. The influence of reaction temperature,reaction time,react-ant ratio and catalyst dosage on product yield were studied. The result showed that the optimum reaction conditions were as follows:α-methoxyformyl-γ-butyrolactone:reaction temperature 25 ℃,reaction time 3 h,n(γ-butyrolactone): n(dimethyl carbonate)= 1 : 1. 5,the amount of catalyst was 0. 3 mol,the yield of the product was ≥85% ;α-carbethoxy-γ-butyrolactone:reaction temperature 30 ℃,reaction time 4 h, n(γ-butyrolactone): n(diethyl carbonate)= 1 : 2,the amount of catalyst was 0. 3 mol,the yield of the product was ≥76% . The products were characterized by 1 H NMR and FTIR.

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乙酯与金属钠反应所生成的碳负离子与碳酸二乙酯反应生成苯基丙二乙酯,经四氢化铝锂还原、酸化得到2-苯基-1,3-丙醇.通过四溴化碳/三苯基膦、硫代酸钾的羟基官能团转化反应,合成2-苯基-1,3-溴丙烷和2-苯基-1,3-丙硫醇,最后用肼还原硫醇,合成了目标产物2-苯基-1,3-丙硫醇.所有中间产物和目标产物经核磁共振氢谱或红处光谱表征.
Condensation of ethyl phenylacetate with diethyl carbonate in the presence of sodium gave diethyl phenylmalonate,whose reaction with lithium aluminum hydride yielded 2-phenyl-1,3-propanediol.After a series of functional transformation in the presence of carbon tetrabromide/triphenylphosphine,potassium thioacetate and hydrazine hydrate,2-phenyl-1,3-propanedithiol had been obtained.

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研究了四氟硼酸四基铵(Et4,NBF4)添加到LiPF6基电解液(碳酸乙(EC)+碳酸二(DMC)+碳酸乙酯(EMC)(质量比为1∶1∶1)对(LiMn2O4+活性炭(AC))/Li4Ti5O12超级电容电池电化学性能的影响.线性扫描(LSV)、循环伏安(CV)及电池充放电等测试结果表明:Et4NBF4盐改变了复合电解液中离子对的结构,提高了复合电解液的高电压稳定性和电导率.在实验条件下,随着复合盐电解液中Et4NBF4含量的增加,电池放电容量也增加,含有Et4NBF4与LiPF6物质的量的比为4∶1的电解液的电池电化学性能最好,在4C倍率下循环5,000周后,容量还有86.8,mA·h,保持率为95.8%.
The effect of blended salts(Et4NBF4 and LiPF6)added to the ethylene carbonate+dimethyl carbonate+ethyl(methyl)carbonate(mass ratio of EC,DMC and EMC is 1∶1∶1)on super-capacitor battery system consisting of LiMn2O4/activated carbon(AC)as the cathode,and Li4Ti5O12 as the anode was investigated. The electrochemical performance of the batteries was tested by linear sweep voltammetry(LSV),cyclic voltammetry(CV) and charge-discharge tests. The results indicate that Et4NBF4 salt charges the structure of ion-pairs,and improves the high-voltage stability and conductivity of composite salts electrolyte. With the addition of Et4NBF4,more free ions are provided,and the capacity of the super capacitor battery increases. It is also found that the battery shows best electro-chemical performance with the mole ratio of Et4NBF4 and LiPF6 being 4∶1,the discharge capacity is 86.8,mA·h and the capacity retention is 95.8%after 5,000 cycles at 4C rate.

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本文以醋酸锂和钛酸丁为原料,以冰醋酸为抑制剂,采用溶胶-凝胶法制备了晶态Li4 Ti5 O12负极材料。与自制的3种电解液和实验室常用的电解液分别组装成锂/钛酸锂半电池。采用恒流充放电测试、循环伏安法(CV)及交流阻抗法(EIS)对其电化学性能进行研究。研究结果发现:在以环状碳酸酯类(EC、PC)和线性碳酸酯类( MEC)为溶剂、以六氟磷酸锂( LiPF6)为电解质的电解液中添加双乙二酸硼酸锂( LiBOB),有利于提高半电池的性能,首次放电比电容达到了198mA. h. g-1,且放电比电容经多次充放电后衰减得较小。而在电解液中加入碳酸( VC),半电池的性能有所下降。 Li4 Ti5 O12对电解液表现出较明显的兼容性。
Lithium acetate and butyl titanate were used as raw materials,glacial acetic acid as inhibitor,nanocrystalline Li4 Ti5 O12 for the anode material of lithium-ion battery was prepared by sol-gel technique. The Li4 Ti5 O12 , three pre-prepared electrolytes and a conventional electrolyte were used to assemble four half-cells Li/Li4 Ti5 O12 , respectively. In order to explore the compatibles of Li4 Ti5 O12 toward the electrolytes, we performed the characterizations of galvanostatic charge-discharge tests, cyclic voltammetry (CV)and electrochemical impedance spectroscopy(EIS)for those half-cells. The research results showed that the performances of half-cell Li/Li4 Ti5 O12 could been improved by adding lithium bis( oxalato) borate( LiBOB) to the electrolyte that consisted of LiPF6, cyclic carbonates(EC,PC),and linear carbonate(MEC). The first discharge specific capacity of the half-cell reached 198mA. h. g-1 with less decrease under 20-time cycles of charge-discharge. However,when

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